Apparatus for the delivering of liquids under pressure



Feb. 5, 1952 W. POOL APPARATUS FOR THE DELIVERING OF LIQUID UNDER PRESSURE 4 Sheets-Sheet 1 Filed May 25, 1946 v Inventor' W-POOL u A ltorneys W. POOL APPARATUS FOR THE DELIVERING OF LIQUID UNDER PRESSURE Feb. 5, 1952 4 Sheets-Sheet 2 Filed May 25, 1946 ltarney Feb 5, 1952 w. PooL APPARATUS FOR THE DELIVERING 0E LIQUID UNDER PRESSURE 4 Sheets-Sheet 3 Filed May 25, 1946 Feb. 5, 1952 w POOL 2,584,226

APPARATUS F'R THE DELIVERING OF LIQUID UNDER PRESSURE Filed May 25, 1946 4 Sheets-Sheet 4 Inventor \N.POOL.

Patented Fei). 5, 1,952

UNIT ED S 'FTA-TES FICEV 2,584,226 APPARATUS Foa 'rHEpE-Llypuilyd or LIQUIDs UNDER PREssri-IRE willie-iii P601, spul-mon, near Derby; Eugenia, as signorto Celane'se Corporation" of Aniia,

corpora-tion of Delaware Application May 2.5, 1946, SerialfNo, fillftgf'l' InGreat Britain J 4, 1945 Claims.

l i This invention relates to" apparatus for the delivering f liquids' under pressure and par-V ticularly to' the delivering of liquidsat a Coristarlt vlumetri rat, and is especially coilcerned with the delivering f liquids having a basis ofY a iibreor nlm-forming substance through extrusion oriees f appropriate shape and size, for the production of artiial fila# ments, foils, lms andrlile materials. A

The problem of maintaining constant the volumetrie rate of extrusic'lnV is one that must be constantly borne inv mind in the production by extrusion of sueh artiiicial products, in order to ensure that the extruded products are of a cross-sectional area that is uniform along their length. Dilerent means may be employedv 'for applying the pressure by Wlicli the liquids Yare extruded.. Thus, the liquids may be extruded bi the application ff an inert gas under pfessur'e'to abody f liquid thati'sfr'ee to escape, by vvay' ci' suitable lters, through the extrusion orifle's.' Constaney ofA the rate of extrusion in this case depends on the co'flstaney of the resistance tof 110W offered by' the lte'rs and; extrusion orifices, and as this is very liable t0 vary in the Course of the extrusion peiation this method is apt to be Very unsatisfactory. Alternatively the" materials may be extruded'by means of a pump carefully designed and constructed inrorder togiv'e a constant ratelof delivery when' driven at a constant speed; Even in this case, however, variationsin the resistance of the lters and spini'iingv orifices' are apt to give rise to some variationinthe rate' of extrusion. To overcome" this diiculty" the pump maybe arranged so as to Workwithie'qual' pressures lon its inlet arid-outlet'sides, auxiliary meal'is beingemployed to supply the'liquid under pressure to thev inlet side'of the pump andliduid being' by-pas'sed fromsaid inletl side back tothe source of supply atsuch arate, under'tlie' joint control'of pressures on the inlet andftheoutlet sides of the pump, as to make thel pressure on theinlet side ofthe-pump equal to that of ther outlet side. An example of suchian arrangement is' descriltiedinV British specification- No'; 182,154, infwhich eacliA measuring pump isv preceded by,V ai pilot pump adapted to'deliver' an excess of liquid" to the* measuring pump, liquid being: by=passed backacross the ,pilot `pumpthrougl'l'favalve autotiiiati'cally controllediin accordance with :the--pres- Sures'on the'delli/'eryY` Sides f the t'W'DuS; It is an object of the pres-eniiilveiitioii to prev-ide afurther improvement in the means aritlz methods for the delivery 0f liqllldsaii CO'Y volumetric ralte'byY means'iof'a measuring pump;

in4 Which improvement the' by'f'pass of' the liquid from theA inlet side` Y a measuring pilfi's fv'i* ed;

Accordingto' the prsent' inventina-nietlid ff delivering a liqiliq ai; a @triste-nt volumetria rate' con'lprises supplying the' liquid undr pr'essi'lrey to a measuring" pump lily'applying'tofaldyl the liquidj an l'leitfluid luider' pieSSir; difiy'g the said measuring* pumpso` t6 deliv liquid, and' adjusting'- tiie pressure ori said 'I fluid under thetcntrolfthe delli/eI Sli in said liquididllthe iltli-'isideVx Off said p as to maintain said in ert fluid pressure substanl tially' equal tds'aid: delivery pressuri' Inl thisl way, trie liquid is metered' from Vtlie'bid'y off liquid, andthe"pressure applied by thiert Huid* iq the body" qi" liquid is adjust-,eq accordance With' the 'pressures ifi thgliqid" immediately bee fore and ir'rlme'diately` after" metiing" so" as te maintain' said'pre'ssure's substantially equal;

ed by it is avided; While inert liquid frias"- extrusion off lament-foririing` liquids,v` and more ,particularly melt-spinning.i.- e. the extrusionef immediately before extrusion and not kept for a long period in the molten condition or transported by pipe lines in that condition to the point of use. For these reasons it is desirable that the materials should be melted in amelting vessel in the immediate neighbourhood at the point of extrusion, a circumstance which makes it convenient to bring about the extrusion of the liquid by applying a gas pressure there-f to, the gas pressure being applied in the vessel in which the materials are melted. Not only can such-.gas vpressure be conveniently applied to the vessel in which melting takes place but also the possibility of causing some parts of the material to remain for long periods in a molten state before being extruded, through repeated return flow and re-circulation of molten material, is avoided. Moreover, it is a considerable advantage to have only one pump, instead of two pumps and a system of by-pass passages and valves, subjected to the temperature necessary to melt the material, which temperature is often very high e. g. of the order of 300 C. or more.V

A further advantage of the invention that applies particularly to melt-spinning is that the material, from the time that itis subjected to melting temperature until the time it is extruded, is vmaintained under a substantial pressure whereby the formation of small bubbles therein,

such as would interfere with Vthe uniformity,

strength and appearance of the extruded products is substantially inhibited. Indeed, it may be advantageous to maintain a higher pressure on the material up to the point of extrusion than would otherwise be necessary, e. g. by the inclusion of extra iilters or throttlingv devices in the path of the material to the'extrusion orifices.

K The control of the gas pressure on the material being extruded may conveniently be effected by supplying gas from a source of supply at a high pressure through a reducing valve, on the delivery side of which the gas is allowed to leak at aV controlled rate to atmospheric pressure. The adjustment of the leak provides means whereby the pressure drop between the high pressure source of supply and the vessel to which it is to be delivered may readily be controlled, the amount of this pressure drop depending on the amount of gas ow through the leak and the setting of the reducing valve. The leak may readily be controlled jointly by the pressure in the liquid on 'the delivery side of the measuring pump and the pressure in the gas actually delivered to the melting vessel. Means may also be provided to cut off the leak entirely in the event that the pressureon the delivery side of the measuring pump fails for any reason. If the pressure on the delivery side of the pump becomes excessively high the leak will be cut off in any case, but further provision may be desirable for stopping the measuring pump altogether in such an event, when the pressure on the delivery side of the pump will fall again.

.The invention may be employed in conjunction with means for feeding fresh spinning material to the body of liquid that is subjected to the gas pressure, so that extrusion may proceed continuously. Thus a pressure lock may be employed that is connected to the source of supply of inert gas,V as described in U. S. Patent No. 2,437,686 or Iit may be such as to be substantially lled bythe charge of composition as described in U. S. Patent No. 2,437,704'. 'Ihe feedingy offresh composition may be automatically controlled in accordance with thelevel of liquid within the melting vessel; l e.-v g. as described fin .British Patent No.

4 573,325 especially when, as described in U. S. Patent No. 2,437,685 the melting of the material is effected by means of a heating liquid in which the solid material is immersed.

By way of example, one form of melt-spinning apparatus employing the method of the present invention will now be described in greater detail with reference to the accompanying drawings in which:

Fig. 1 is a diagrammatic side elevation showing the layout of the apparatus as a whole.

Figs. 2 and 3 are details of the hopper feed mechanism shown in Fig. 1.

Fig. 4 is a side elevation in section of the melting and extrusion vessel.

Fig. 5 is a section of a detail of Fig. 4.

Fig. 6 is a sectional plan View, and

Fig. 7 a complete plan view of the melting and extrusion vessel shown in Fig. 4.

Figs. 8 and 9 are a side elevation and a plan view of a detail of Fig. 4,

Fig. 10 a section of a melting and extrusion vessel showing a further detail of the flow control means and an alternative method of heating the vessel, and

Fig. 11 is an enlarged view of a detail of Fig. 8.

Referring to Fig. 1, the apparatus shown therein is a double-sided machine, although only the left-hand side isshown except for the details at the top of the machine.

The machine comprises a general frame-work I carrying on each side a series of melting and extrusion vessels 2 (of which only one is visible in'Fig. 1) of the kind described in BritishPatent No. 573,325 and U. S. Patent No. 2,437,704. The vessel 2 is fed with solid filament-forming material in the form of short sticks supplied from a hopper 3 by way of a tubular chute' 4 and through a feeding mechanism 5 of the kind particularly described in British Patent No. 573,325. Filaments 6 extruded from the bottom of the vessel 2 pass through a tubular-cell l, 8 in which they solidify. The filaments then pass round a guide plate 9 and a guide I0. and on to a collecting roller I I. The guide plate 9 is in the form of a nat horizontal plate having a deep V-notch in its right-hand edge, the angle 'of which constitutes the guide for the laments 5. The plate 9 can be drawn out by means of a handle I2 so as to allow the filaments to fall freely through the tubes 1, 8 on starting. Any casual drops o1' splashes of the filament-forming material falling through the tube 8 in the course of starting collect on the plate 9 and are scraped oi by means of the scraper I3. The cellv l, S is telescopic, the upper part 8 being mounted on guides I4, so that it can be slid downwards, inside vthe lower part l and give access to the bottom of the vessel 2.

The hopper 3 froml which the sticks of larnentforming material are supplied comprises a pair of oblique plates I5, the lower edges of which do not quite meet, but leave a slot through which rises and falls a vertical plate I6. A series of such hoppers is provided, one for each vessel 2, and the several plates I6 thereof are operated by means of a bar I1. The two bars I'I on the two sides of the machine are connected to one another by means of chains I8, which pass round pulleys I9, 20. The upper pulley' I9 is rocked to and fro by means of an eccentric 2I and connecting rod 22 driven through gears 23 from a shaft 2li. In this way the plates I6 are caused to rise and fall. The plate I6 is hollow beingformed of two sheets of metal, and its upper edge is constituted by a quadrant .25 pivoted inside plate I8 about.

` screw-threaded for this purpose.

lindrical cavity is generally indicated at 45 ges-agraciaf pinA 26 and adapted tol swing, whenl the plateV |6- reaches its uppermost position, so asY tobring the upper edge of the quadrant 25i-intoalignment withrthechu-te 4. Thedetails of themechanism for this purposeare shown in Figs. 2- and. 3.: The pivot pin 26 extends through a. slot 7.17.` in the quadrant 25. As the platel I6 rises the upper front corner'oftheduadrant125 engages, asfshown- Fig. 2; with a rocking member 28 p'ivotedl at- 29sand= loaded by meansV ot a springf 36.d The conf-` tinuedv movement of the plate |61, as shown in'y Fig. 3'; causes the quadrant 25i and member; 28. toA tilt-.about 29 so that the upper edgeof the quadrant is in alignment withthe chute- 4. Each time the plate I6 rises it picks-up' a stick of' ma.-V teri'al, with which the hopper spaceoetween the plates l is -11ed','andtiltsl itl intothe chute*I form a-t they top-and of conical form at the bot--l tomr and is formed inY the upper partof the cylindrical steel vessel-"321. From the apex' 35!J ci the` conical part of the chamber 3| a passage leads to a cylindrical metal block 34 constituting the lower part of the vesselV 32,which is securedto` the upperr part by means. of` bolts`35l (Fig. 6) and' containing, in suitablecavties formed' therein, thespinning pump, the spinning jet andI iilters and associated parts, and the pressure-sensitive means by which the rate of extrusion is'controlled. The spinning pump 36 is a gear pump in the form of a cylindricalblock of metal horizontally divided intoithree parts, the middle part beingv cut away to accommodate the gears 3l.

The spindles 38 of the gears extendverticallyintav bearings in the upper and-lower parts" ofv the cyllindrical block, one spindle 33- extending completely through the lowest division of the blocl: byway of a gland 40; and emerging from the bottom tolserve as the driving shaft for the-pump. v The spinning jet 4i and lters 4:2',.as shown in Fig. 4, are ttedv into a second cylindrical cavity 43 inthe block 34, thecavity 43 being internally The third. cy-

Fig. 4 but is shown in greater detail in Figs. 5- and Fig. 6 is a sectional plan view in which is the horizontal centre line of th-e :cavity llfif.` The remainder ofthe section, however,A surround-y ing the block 34, is taken at a lower level to show the means for driving the pump 36. Each ci these three figures shows the fluid connections within the block 34. An inlet hole 50 inthe top tom of the cavity 45 withthe. top of the. cavity` 43 containing the iilter andjetassembly All., 42..

The spinning pump 36` is` driven, as; shown in; Figs. 4l 5 and 6, bymeans of a ,worin 56mounted on a horizontal .Shaft 51;. Pivoted;aboutgthe'axisf of-lthe: shaft 57|: incbearingst 58; 59;screwed;to the. bottomr plate 66 ofl the vessel. 2i is a horizontal framework 6|; in which is journaled-.thelower end oi a. short shaft;62` carrying a worm gear 63. A slotted yoke 64a on theupper faceiofY thewormv gearl 63 receives the squared lower end` of the` pump shaft 39, formingy a dogfconnection which can be. broken by swinging theaframe 6 down-Y wards'. about the wormi shaft.5|:. The wormgear 63: constantly engages: the worm 56,. whatever" the position of' the framev 6|.V The frame-61| also; carriesl a. funnel-shaped shield. 66 lying directly.y below the jet,4|- and serving to. protect filaments emerging from. the jet from draughts. A screw. 61' mountedl onv the frame 6| passes through a key-holel cavity in` a bracket 63 secured to: the bottom platey 6E! and', when screwed home mainftainsthe: frame in its working position. When the-screwV 61 is partly unscrewed, however, a nar'- f row portion 63 thereof-f registers with the keyhole cavity and permits the frame 6| to be swung downwards, giving access to the bottom of the block 34.

The worm 56is drivenl bythe worm shaft 57| bymeans of a dog clutch 16, one member of which is formed integral with the worm,'whiletheother issecured to the worm shaft 5l by means-of a pin H The dog clutch 'Hl is held in eng-agement byfmeans of a collar l2 into which one end of the worm shaft 51 is journaled. Thel shaft 51 is also journaled in the bearing` 59. The collar 'l2 isfjo-urnaled in the bearing 56vand has formed on its outer surface a double turn of deeply-cut screw-thread '13, as Shown in Fig. 5. The screw thread'ls is engaged by a tooth Mon the end or aV spring plunger 'l5 carried*l in an extension i6 of'the frame 6|. The collar 12 extends past the bearing 58 in the form of a shaft 11 and has gear teeth 'I8 formed on its free end which engage with a rack 'I3 formed on a horizontal plunger 86 which slides in bearings 8| in the frame 6|.

Through these means the measuring pump 36 is driven by driving the Worm shaft 5'1, which is done, as shown in Fig. 1by a chain drive 63 from the main shaft 84 of the machine, from which alsoL the shaft 24' is driven by chain 85. If, however, the pump 36 encounters undue resistance so-that the worm gear 63 cannot'rotate, the continued rotation of the worm 56 drives the worm away from the clutch 10 until the clutch is' dis- Gil the/line of section over thearea of the block 34 engaged. This also moves'the collar 12 axially,

the tooth 14 riding over the screw threads 13 until nire-engages withthe next thread, when it serves to hold the clutch 10 out of engagement. The driving of the pump 33 may also-be stopped by hand by pressing the knob 86. of the plunger 86, the collar 'I2 in this case being rotated so as to move axially under the influence of the tooth Mengaging thethread 'E3 ,and to allow the clutch.

Hlttoidisengage. The pump 36. may be restarted byy forcing in the plunger 86 (if ithas not valready been forced in to stop the pump by hand) and withdrawing it-so as tore-engage the worm clutch. v

Thepump 36 delivers molten material through the passage 53. to thecavity 45. The cavity is in the form of a shallow cylinder lhaving at theLbottom a steep-sided, nat-topped boss 96y provided with two concentric,annularridges 9|. The deliyeryv passage 53.r emergesv through the topf of theboss 96. close tothe upper edge thereof, and the passage 54 communicating with the lter 4.2 emerges.` through the, top of: the. boss 36 close. to its: lower.r edge..

The.- pressure.- sensitive,- element. comprises a..

massages T dat', crcuar diaphragm 93 mounted at the bot'- tom of a short cylinder 94 having internal and external flanges 95, 96. The inside of the cylinder 94 is screw-threaded and the diaphragm 93 is nipped against the internal flange 95 by means of a screw-threaded plug 91. The inner face of the plug is recessed to form a at, conical space between the plug and the diaphragm, and the plug is axially bored to receive a pressure tube 98 communicating with this space. The inner flange 95 ts closely round the boss 90 s0 as to enclose a flat, circular space between the face of the boss 90 and the diaphragm 93. The diaphragm is kept just out of contact with the tops of the annular ridges 9| by means of a hard packing ring 99 tting about the boss 90 in the bottom of the cavity and engaged by the inner flange 95. The outer ange 96 is engaged by a ring screwed into the cavity 45 so as to hold the entire pressure sensitive element firmly in place.

In the operation of the device the passages 52, 53, 54 and the space between the boss 90 and the diaphragm 93 are filled with the material to be extruded on its way from the pump 36 to the jet 4|. The space between the diaphragm 93 and the inner face of the plug 91, and the pressure tube 98 communicating with that space, are lled with an appropriate incompressible fluid, e. g., petroleum jelly.

Referring now particularly to Figs. 4 and 7, a high-pressurer main |0| supplies an inert gas under pressure, e. g., hydrogen or nitrogen, to the top of melt chamber 3| by way of a sensitive needle valve |02 and a leak assembly |03 which is shown in greater detail in Figs. 8, 9 and 10. Each of the elements |02, |03 oifers a substantial and adjustable resistance to the flow of gas.

The needle valve |02 is of conventional construction. The leak assembly |03 comprises a thick-walled chamber |04 divided into two parts by a diaphragm |05 firmly clamped at its edges. The space |06 below the diaphragm communicates, by way of the pressure tube 98, with the pressure-sensitive element in the cavity 45, and is lled with the same incompressible uid. The

part |06 of the chamber |04 also communicatesl with a pressure gauge as indicated at |01. The part of the chamber |04 above the diaphragm |05 contains a plate |09 centrally secured to the diaphragm, the surface of the plate |09 lying close to the edges of a conical nozzle I0 entering the chamber |04 centrally from above. The line from the needle valve |02 enters the chamber |04 above the diaphragm |05, and the line ||2 leading to the melt chamber 3| leaves the chamber |04 from above the diaphragm, both passages being offset from the axis of the chamber |04, as shown in Fig. 9. The line ||2 enters the top of the chamber 3| at ||3. Leakage of gas passing from the needle valve |02 to the melt chamber 3| takes place through the'central nozzle ||0, the leaking gas is led away through the pipe ||4. If desired, the pipe ||4 may be led down and deliver the leaking gas inside the funnel shaped shield 66, so as to keep the hot laments emerging from the jet 4| in an inert atmosphere, and prevent their oxidation. The rate of leakage through the nozzle I0 is cont-rolled by the position of the plate |09 in relation to the edge of the nozzle ||0.

When the pressure on the delivery side of the measuring pump 36 is high, the pressure in the lower part |06 of the leak assembly |03 is also high, so that the diaphragm |05 and plate |09 are raised. In consequence, the leak throughv the nozzle ||0 is diminished by the approach of the plate |09 to the edge of the nozzle. This leak'- represents substantially the whole of the flow taking place through Vthe needle valve |02, and

its diminution diminishes the pressure ,drop

across the needle valve. This raisesv the pressure in the melt chamber 3| and that in the upper part of the leak assembly chamber |04 to a value more nearly equal to the pressure within the main |0 I. When these pressures are substantially equal to the pressure on the delivery side of the measuring pump 36, which is also the pressure in the space |06, a balance is achieved. The resistance to deflection of the diaphragms 93 and |05 is low, so that the pressure difference in each case required to bring about the deflec-l tion necessary to balance the pressures on the inlet and outlet sides of the pump 36 is negligible in relation to the magnitude of those pressures. It will be seen that the diaphragms 93, |05 `act in unison, on account of the incompressible iluid enclosed between them, so that it would be possible to control the rate of leak by disposing the nozzle ||0 close to the face of the diaphragm 93, and omitting the diaphragm |05 altogether. The arrangement shown, however, is more convenient in construction, assembly and operation.

In order to prevent undue leakage of gas in the event of failure of therpump 36, a cut-oil" valve is provided adapted to act when the pressure on the delivery side of the pump 36 falls unduly. For this purpose, a valve rod 5 is providedrcentrally upstanding from the plate |09 and passing up through the nozzle ||0. The upper end of the rod ||5 carries a valve member ||6 adapted to engage with a conical seating in the passage by which gas escapes through the nozzle I0. When the pressure on the delivery side of the pump 36 and therefore in the lower part 06 of the chamber |04 falls, the plate |09 drops to such an extent as to bring the valve member I6 down on its seating, thus cutting 01T the leak altogether. In

this way, the gas pressure in the melt chamber 3| is prevented from falling off in the event of the failure of pressure on the delivery side of the measuring pump 36.

Since the pressures on the inlet and outlet sides of the pump 36 are substantially equal, the pump is enabled to act accurately as a measuring pump, to deliver liquid at a constant volumetric rate to the filter y42 and jet 4|. The power necessary to force the liquid through the lter and jet is derived not from the pump 36 but from the gas supplied at high pressure from the gas main |0| to the top of the chamber 3|.

The gas supplied at |3 to the top of the chamber 3| acts on the upper surface of a heating liquid which is not the liquid to be extruded but serves to melt solid material introduced into the vessel 3|. The solid material is heavier than the liquid and sinks through it until it reaches and is retained by a conical grid ||8 as described in U. S. Patent No. 2,437,687, by which it is conducted to the walls of the chamber and is melted by convection currents induced in the liquid by the supply of heat through the walls of the vessel. The molten material forms a pool ||9 in the conical bottom of the chamber. For supplying heat through the walls of the chamber 3|, the vessel 32 in which the chamber is formed is surrounded by a jacket |20 containing a molten alloy of equal parts of tin and lead |2| and heated by means of electrical heating elements |22 supplied with powerby connections |23 from la power conduit '|34 through the bracket 3S.' `Auxiliary heatingelements |24 are provided round the top ange of the vessel also supplied from the power conduit |34. The supply of power to the windings |22 is controlled in accordance with a temperature-sensitive instrument |25 emerging from the top of the vessel and dipping into the alloy |2| at |26. The feed of solid material to the melt chamber 3'| is controlled, as described in British Patent No. 573,325, by means of a atbased conical bulb |21, the base of which is situated at the level of the heating liquid As the fused filament-forming material, collected at ||9 in the conical bottom of the chamber 3|, is drawn off for extrusion, the level of the liquid falls. Between the liquid and the gaseous phase above it, there exists a temperature. difference so that, as the level of the liquid ||7 falls, a temperature change isexperienced by the temperature-sensitive element |21. This temperature change' is utilised, as described in U.,S. Patent No. 2,437,704, to feed further. solid material through thefeed mechanism and the passage |28. A valve rod |29 operated by a hand-wheel |30 is provided to close the passage ,33 to the molten material ||9 when desired, and a second valve rod |3| operated by wheel |32 is provided in a bore in the rod |29, to permit the passage of heating liquid through 33 by way of ports |33 and valve rod |29, for the purpose of starting up.

Fig. 10, besides showing a different section through the block 34 fromfthat shown in Fig. 4, shows an alternative method of heating the Vessel,32. In this case the vessel 32 is surrounded by a pressure-tight jacket |35 heated at the bot- Vtom by electrical heating elements S33 and conl taining a liquid having a suitable range of boiling points under different pressures, e. g. a mixture of diphenyl and diphenyl oxide. The control of -the temperature in the jacket |35 is brought about by controlling the supply of heat so as to keep the pressure constant. A pressure lead |38 leads to a pressure-sensitive element by means of which the power supplied to the heating element |36 is readily and accurately controlled, without the necessity of `complicated and delicate relays and the like, the pressure itself supplying ample power for the purpose.

As stated above, the invention is applicable to the delivery of liquids generally at a constant volumetric rate and particularly to theV extrusion of filament-forming liquids, and more particularly to the extrusion of fused filament-forming materials. Examples of materials that may be extruded in the fused state are the synthetic linear polyamides made, for example, by the condensation of diamines with dicarboxylic acids, and polyvinyl compounds, for example polyvinylidene chloride and copolymers of vinyl chloride and vinyl acetate. Other lament-forming liquids that may be extruded are solutions in volatile solvents of cellulose derivatives, such as organic esters of cellulose (including mixed esters) e. g. cellulose acetate, cellulose propionate, cellulose butyrate, cellulose acetate-butyrate, cellulose acetate-propionate and cellulose acetate-stearato, or cellulose ethers such as ethyl and benzyl cellulose.

Having described my invention, what I desire to secure by Letters Patent is:

1. Apparatus for delivering a liquid at a controlled volumetric rate, said apparatus comprising a pressure vessel for .containing a supply of liquid, a measuring pump connected to said vessel for delivering said liquid therefrom, meansrfor supplying under pressure to -said vessel a uid different from-the liquid to be delivered, pressure-,sensitive means subject to pressure differences between the inlet and outlet of said pump, and means under the controlof said pressuresensitive means for varying the pressure ofsaid iiuid so as to maintain said pressure-difference substantially null, whereby said pump is enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure differencesbetween the inlet and the outlet of said pump. I l

A2. Apparatusfor delivering a liquid' at a controlled volumetric rate, said apparatus comprising a pressure vessel for containing a supply `of liquid, a .measuring pump. connected to said' vessel for delivering rsaid liquid therefrom,means for supplying under pressure to said vessel a iiuid different from the liquid to be Udelivered,and pressure-sensitive means comprising adiaphragm that is subjected on one sideto the pressure on the delivery side of V'said pump and onthe other to the pressure insaidpressure vessel and adapt,- ed, by movement under a diierence between said pressures, to control the .supply-pressureof said fluid so as to maintain said difference substantially null, whereby said pump is enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump.

3. Apparatus for delivering aliquid 'at a controlled volumetric rate, said apparatus comprising a pressure vessel for containing a supply of liquida measuring pump connected to said vessel for delivering said liquid therefrom, a conduit for connecting said pressure vessel to asource of supply of inert fluid under pressure, .a resistance to 'uid ow in saidconduit, an outlet .in .said conduit between said resistance and said pressure -vessel forv permitting leakage of said fluid, pressure-sensitive means subject to pressure differences betweenL the inlet and the outlet vof said pump, and means under the control ofsaidpressure-sensitive means for controlling the, rate of said leakage-so as to varythe pressure dropacross said resistance and ,thereby ther pressure applied in said vessel through said conduit and to maintain said pressure-difference substantiallynull, whereby said pump is enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump. e

4. Apparatus for delivering Ya liquid at a controlled volumetric rate, said apparatus' comprising a pressure vessel for containing a supply of liquid, a measuring pump` connected to said vessel for delivering said liquidtherefrom, a. conduit for connecting said pressure vessel to a source of supply of inert fluid under pressure, a resistance to uid flow in said conduit, a nozzle pointinginwards into said conduit between said `resistance and said pressure vessel for permitting 'a leakage of said fluid, and a diaphragm subjected on one side to the pressure on the delivery side of said pump and on the other tothe pressure in said conduit, said diaphragm being. closely spaced from the mouth of said nozzle so as to control the rate of said leakage and thereby the pressure drop across said resistance, whereby the pressure applied in'said vessel through said con- -duit is maintained substantially equal to the pres,- sure on the outlet side of said pump andsaid pump is enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure l1 dinerences between the inlet and thev outlet of said pump.

5. Apparatus for delivering a liquid at a controlled volumetric rate, said apparatus comprising a pressure vessel for containing a supply of liquid, a measuring pump connected to said vessel for delivering said liquid therefrom, a conduit for connecting said pressure vessel to a source of supply of inert fiuid under pressure, a resistance to iluid flow in said conduit, a nozzle pointing inwards into said conduit between said resistance and said pressure vessel for permitting leakage of said iiuid, and a pair of diaphragms having an incompressible iiuid enclosed between them, one of said diaphragme being subiected to the pressure on the delivery side oi said pump and the other being subjected to the pressure in said conduit and being closely adjacent to the mouth of said nozzle so as to control the rate of said leakage and thereby the pressure drop across said resistance, whereby the pressure applied in said vessel through said conduit is maintained substantially equal to the pressure on the outlet lside of said pump and said pump is enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump.

6. Apparatus for delivering a liquid at a controlled volumetric rate, said apparatus comprislng a pressure vessel for containing a supply of liquid. a measuring pump connected to said vessel for delivering said liquid therefrom, a conduit for 'connecting said pressure vessel to a source of suonlv of inert fiuid under pressure. a resistance to fluid flow in said conduit. an outlet in said conduit between said resistance and said pressure vessel for permitting leakage of said fluid, pressure-sensitive means subiect to pressure differences between the inlet and the outlet of said pump. means under the control of said pressuresensitive means for controlling the rate of said leakage so as to vary the pressure drop across said resistance and thereby the pressure applied in said vessel through said conduit and to maintain said pressure difference substantially null, whereby said pump is ,enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump. and means for closing said leakage outlet onfailure of the pressure on the outlet side of said pump.

'7. Apparatus for delivering a liquid at a controlled volumetric rate, said apparatus comprising a pressure vessel for containing a supply of liquid, a measuring pump connected to said vessel for delivering said liquid therefrom, a conduit for connecting said pressure vessel to a source of supply of inert fluid under pressure, a resistance to .fluid flow in said conduit, a nozzle pointing inwards into said conduit between said resistance and said pressure vessel for permitting a leakage of said iiuid, a pair of diaphragms having an incompressible fluid enclosed between them, one of said diaphragms being subjected to the pressure on the vdelivery side of said pump and the other being subjected to the pressure in said conduit and being closely adjacent to the mouth oi said nozzle so as to control the rate of said leakage and thereby the pressure drop across said resistance, whereby the pressure applied in said vessel through said conduit is maintained substantially equal to the pressure on the outlet side of said pump and said pump is enabled to deliver said liquid at a controlled volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump, a valve stem mounted on said diaphragmV and entering'said nozzle, and a valve member mounted on said stem within said nozzle and adapted, on failure of the pressure on the delivery side of said pump and consequent motion of said diaphragm away from said nozzle, to close said nozzle.

8. Apparatus for the extrusion of lamentforming liquids said apparatus comprising a pressure vessel for containing the liquid to'be extruded, a measuring pump connected to said vessel for delivering the liquid therefrom, an extrusion orifice connected to and adapted to be supplied by said pump, means for supplying under pressure to said vessel a fluid dierent from the liquid to be delivered, pressure-sensitive means subject to pressure diierences between the inlet and the outlet of said pump, and means under the control of said pressure-sensitivefmeans for varying the pressure of said fluid so as to maintain said pressure-dierence substantially null, whereby said pump is enabled to extrude said filament-forming liquid at a constant volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump.

9. Apparatus for the extrusion of filamentforming liquids said apparatus comprising a pressure vessel for containing the liquid to be extruded, a measuring pump connected to said vessel for delivering the liquid therefrom, an extrusion orifice connected to and adapted to be supplied by said pump, a conduit for connecting said pressure vessel to a source of supply of inert fluid under pressure, a resistance to iiuid flow in said conduit, a nozzle pointing inwards into said conduit between said resistance and said pressure vessel for permitting leakage of said fluid, and a pair of diaphragms having anV incompressible fluid enclosed between them, one of said dia,- phragms being subjected tothe pressure on the delivery side of said pump and the other being subjected to the pressure in said conduit and being closely adjacent to the mouth of said nozzle so as to control the rate of said leakage and thereby the pressure drop across said resistance, whereby the pressure applied in said vessel through said conduit is maintained substantially equal to the pressure on the outlet side of said pump and said pump is enabled to extrude said filament-forming liquid at a constant volumetric rate undisturbed by pressure differences between the inlet and the outlet of said pump. Y

10. Apparatus for the extrusion of filamentforming liquids said apparatus comprising a pressure vessel for containing the liquids to be extruded, a measuring pump connected to said vessel for delivering the liquid therefrom, an extrusion orifice connected to and adapted to be supplied by said pump, a conduit for connecting said pressure vessel to a source of supply of inert fluid under pressure, a resistance to iiuid flow in said conduit, a nozzle pointing inwards into said conduit between said resistance and said pressure vessel for permitting a leakage of said liiuid, a pair of diaphragms having an incompressible fluid enclosed between them, one of said diaphragms being subjected to the pressure on the delivery side of said pump and the other being subjected to the pressure in said conduit andrbeing closely adjacent to the mouth of said nozzle so as to control the rate of said leakage and thereby the pressure drop across said resistance, whereby the pressure applied in said vessel through said conduit is maintained substantially equal to the pressure on the outlet side of said .13 Y 14 n pump and said pump is enabled to extrude said REFERENCES CITED filament-forming liquid at a constant volumetric The following references are of record in the rate undisturbed by pressure differences between l of this arent: the inlet and the outleti of said pump, a valve stem e p mounted on said diaphragm and entering said' 5, UNITED STATES PATENTS nozzle, and a valve member mounted on said Number Name Date stem within said nozzle and adaptedI on failure 1,731,231l Hillebrand Nov. 11, 193D of the pressure on thejfdelvery side of said pump 1,993,790 Kinsella Mar. 12, 1935 and consequent motion of said diaphragm away from said nozzle, to close said nozzle.

WILLIAM POOL. 

